US6474420B1 - Device and method for controlling fire - Google Patents

Device and method for controlling fire Download PDF

Info

Publication number
US6474420B1
US6474420B1 US09/634,622 US63462200A US6474420B1 US 6474420 B1 US6474420 B1 US 6474420B1 US 63462200 A US63462200 A US 63462200A US 6474420 B1 US6474420 B1 US 6474420B1
Authority
US
United States
Prior art keywords
fire
controlling
catalytic
screen
flame
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
US09/634,622
Inventor
Kayyani C. Adiga
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to US09/634,622 priority Critical patent/US6474420B1/en
Application granted granted Critical
Publication of US6474420B1 publication Critical patent/US6474420B1/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • AHUMAN NECESSITIES
    • A62LIFE-SAVING; FIRE-FIGHTING
    • A62CFIRE-FIGHTING
    • A62C8/00Hand tools or accessories specially adapted for fire-fighting, e.g. tool boxes
    • A62C8/06Fire-blankets

Definitions

  • This invention relates to a device and method of suppressing fire plumes above combustible structures. More particularly, the present invention relates to controlling and suppressing fires by inserting a catalytic screen into the fire and diverting the reactions from the violent flame zone to a silent catalytic solid surface.
  • the hot flame above the burning object acts as an aerodynamically strong diffusion pump powered by natural buoyancy forces.
  • Ambient air is entrained along the boundary of the flame because of the upward movement of hot combustion gases caused by the large buoyancy forces.
  • the violence of the fire thus depends on the buoyancy force generated by hot gases rising above the fire and the ambient air rushing into the fire. More often than not, crosswinds augment the fire violence.
  • the flame turns into a propagating large-scale fire with ever increasing strength and ability to destroy nearby combustible objects. Out of control fires cause severe threats to both life and property at an ever increasing rate. Thus, a critical need exists for newer and more efficient fire control methods.
  • Chemical additives include, but are not restricted to, the halons CF2Br2 and CF2BrCl, and certain dry powders. Additionally, some explosive reactions are used to aerodynamically blow off the flame and assist in suppressing the fire.
  • U.S. Pat. No. 5,158,144 issued to Mark D. Shaw and Laurence M. Bierce on Oct. 27, 1992 teaches a method of creating a non-burning zone at the flame base by introducing a non-catalytic metal mesh or screen. By constantly raising the screen, a distance of free flowing fuel without fire can be created below the flame. The screen thus prevents the fire from burning below it mainly due to the aerodynamic effect. However the screen does not modify the properties of the flame burning above the screen.
  • catalytic combustion technology exists in several camping accessories, household appliances and industrial combustion systems. In these existing applications, catalytic combustion technology is used to replacing flaming combustion with catalytic radiant glow to create flameless combustion applications for cooking, heating, and improving efficiency.
  • prior art does not exist with respect to the application of catalytic combustion technology for suppressing and controlling violent fires.
  • flaming gas phase combustion will transition to glowing surface combustion in the presence of a significantly lower activation energy catalytic surface.
  • a fire is controlled by transforming the gas phase combustion of a violent flame into a surface catalytic combustion process, thus weakening or eliminating the violent fire plume above the burning structures.
  • the gas phase ignition temperature of a combustible mixture containing a gaseous fuel and air is generally above 1000° C.
  • the fuel-air mixture can ignite at a much lower temperature because of lower activation energy of combustion.
  • the ignition temperature can be as low as 400-500° C. depending on the nature of the catalyst.
  • FIG. 1 depicts a typical fire plume above a burning object.
  • FIG. 2 a illustrates a catalyst coated mesh screen of the present invention inserted at the flame base and having a reduced flame and a glowing surface.
  • FIG. 2 b illustrates a cut-away top view of a catalyst coated mesh screen as shown in FIG. 2 a inserted at the flame base and having a reduced flame and a glowing surface.
  • FIG. 3 a and FIG. 3 b illustrate a catalyst coated mesh screen of the present invention inserted at the flame base and having a glowing surface.
  • FIG. 4 illustrates multiple screens stacked onto a flame base.
  • FIG. 5 shows a plurality of screens spread over a flame base to cover a wider area of fire.
  • FIG. 6 illustrates a catalyst coated screen of the present invention having a mesh structure with impermeable regions.
  • FIG. 7 illustrates a honeycomb substrate structure coated with catalysts as an alternative embodiment of the present invention.
  • FIG. 8 illustrates as an alternative embodiment of the present invention a combination of a mesh catalyst screen structure and a honeycomb substrate structure coated with catalysts.
  • FIG. 9 illustrates a means of inserting the catalyst coated screen into a flame base.
  • FIG. 1 shows a fire plume 2 established above a burning object 4 .
  • the burning object 4 is also considered a source 4 of fuel gas flow 6 .
  • the source 4 can be either gas or gaseous products produced from a condensed phase.
  • the condensed phase includes solids, liquids, or a combination thereof.
  • the fuel vapors from the burning object 4 rise into the upward flowing fire region as shown by fuel flow 6 and keep the fire 2 burning.
  • the air entrainment process 8 in a typical fire plume 2 is indicated in FIG. 1 by a downward arrow 8 .
  • the flow inside a moderate and large-scale fire 2 is highly turbulent. Air and fuel vapors meet and burn instantaneously at locations 10 at the fire's boundaries as a diffusion flame. The combustion process in fires is usually diffusion-controlled. Chemical reaction rates are generally high.
  • the hot gas phase above the fuel source 4 referred to as fire 2 , is generally about 1600-2000° C. Depending on the fire size and crosswind conditions, the fire 2 moves violently at all sides and attempts to bounce onto nearby combustible objects.
  • a mesh material or a screen 12 is placed across the base 14 of the fire as shown in FIG. 2 a and FIG. 2 b .
  • the screen 12 is coated with a catalytic material and is also referred to as a catalytic screen, catalytic screening member, or a fire-suppression screen 12 .
  • the catalyzing process begins, and the screen 12 quickly heats up to its activation temperature, which is lower because of the catalytic coating.
  • the fuel-air mixture ignites at a temperature as low as 400-500° C. because of lower activation energy caused by the combustion catalyst. When the catalyst is heated to above its activation temperature, combustion reactions occur on the surface of the screen 12 .
  • the catalytic screen member 12 is heated to its activation temperature during its descent to the fire's base 14 .
  • the catalytic screen 12 is immediately hot enough to cause surface combustion reactions and begin the transition to surface glow.
  • the oxygen of the air entrainment process 8 and fuel vapor of the fire 2 react and release heat producing a glow as shown at the reaction point 16 .
  • Both the reduced flame 18 and initial glow reaction 16 are seen immediately after inserting the screen 12 .
  • the glowing region follows the shape of the fuel as shown by reaction point 16 in FIG. 2 b . This is because the oxygen and fuel meet the screen 12 at the locations where the temperature of the screen 12 is above the catalyst activation temperature. At the center of the screen 12 , a weak flame 18 may persist. If the screen 12 is fine enough, the fuel flow 6 will be partially blocked from rising above, and the flow will go sideways and meet the oxygen at the edge of the screen 12 .
  • FIG. 3 a and FIG. 3 b show the transition from the residual fire 18 in FIG. 2 a to a glowing surface 20 with a temperature about 1000° C.
  • the placement of the catalyst coated screen 12 into the base 14 of the fire plume 2 causes the fire 2 to transition into a glow 20 that replaces the fluid dynamically strong, and violent fire plume 2 depicted FIG. 1 .
  • the glow is less violent, the reaction event is much safer and manageable.
  • the glow will not ignite nearby objects as a violent flame 2 will.
  • the glow 20 is easily extinguished by cooling the glowing surface with a standard system of dispensing water onto the surface.
  • other fire extinguishing chemicals, fluids, solids, or methods may be applied to the glow 20 and will generally be highly successful in extinguishing the non-violent glowing surface.
  • FIG. 4 describes a typical multiple mesh system 22 to obtain an effective transition from fire 2 to surface glows 20 .
  • the physical size of the screen 12 and its orientation depends on the fire scale and intensity.
  • several screens including a catalytic screen 28 and non-catalytic screen 30 are shown stacked vertically.
  • the vertically stacked arrangement of multiple screens may be useful in cases of fires 2 having very strong upward flow 6 .
  • the vertically stacked screens will provide several reactive surfaces such as the reactive surfaces 16 in FIG. 2 b . Multiple reactive surfaces may assist in controlling the fire 2 and causing the fire 2 to transition into catalytic surface glow 20 on the screens.
  • the alternate mesh 30 may be a simple mesh without a catalytic coating.
  • random patches of impermeable regions 32 may be used on a mesh as shown in FIG. 6 to block the upward flow 6 and accelerate the transition to surface glow.
  • a honeycomb structure 24 may be used as shown in FIG. 7 .
  • the depth of the honeycomb channel 26 in FIG. 7 may be suitably dimensioned to get an optimum fire transition result. It is also possible to use a combination of a screen 28 and a honeycomb structure 24 as shown in FIG. 8 .
  • the position and dimensions of the screen 12 are optimized for each fire scenario based on the magnitude of the area and flow 6 of the fire 2 .
  • several units of individual screens 12 may be combined and linked together as illustrated by FIG. 5 .
  • the screens 12 may be retained against the fire base 14 by their own weight, or further support may be added depending on the specific fire scenario.
  • weights 18 may be added to hold the screen 12 in place against the upward fire flow 6 .
  • Various wheels and pulleys and equipment such as cranes, lifts, or aircraft may be used to position screens in certain fire scenarios.
  • a possible scenario using an aircraft 34 to place multiple catalytic screening members 12 at the source 4 of a wildfire 2 is illustrated in FIG. 9 .
  • Catalytic materials for coating the screen 12 may include platinum, palladium and their alloys, transition metal oxides, and other low temperature oxidation catalysts.
  • the alloys of the these metals may be used for more effective catalyst performance.
  • a catalyst having a composition with an extremely low activation or light off temperature is desirable to cause a quicker transition from fire to glow.
  • the surface reactions caused by the combustion catalyst may be further accelerated by supplying additional air or oxidizing chemicals to the surface of the catalytic screen 12 .
  • catalysts are coated on a substrate material or screen 12 of sufficient mechanical strength.
  • the substrates may also be called catalyst support materials.
  • the catalyst will very thinly coated on the substrate.
  • a thin coating of the catalyst is still be effective and cost efficient.
  • the known process of modem chemical vapor deposition (CVD) or any other thin-coating method may be utilized to formulate an efficient catalytic screen. After a reasonable number of fire control applications, the catalytic surface of the screening member is regenerated. Similarly, after the catalytic surface become ineffective, it may be re-coated with the catalyst.
  • CVD modem chemical vapor deposition
  • Typical substrates may include metal screens or meshes, honeycomb structures, or a foam-like network.
  • Other non-combustible materials and fibers that may be used as substrates include ceramic foam, a non-oven carbon mat, graphitic felt, carbon fiber yarn, carbon felt, woven ceramic fibers, fiberglass mats, and monoliths, also referred to as honeycombs.
  • Various substrates may be used and the list provided is not intended to be all inclusive.
  • the substrate and catalyst of the screening member may be combined or the same material rather than having a substrate that is coated by a separate catalytic material. Obvious variations and combinations of both catalytic coatings and substrates will become apparent to those skilled in the art.
  • preferred embodiments of the invention will consist of very fine stainless steel screens of grid size 0.1 mm and wire diameter 0.2 mm.
  • the preferred grid size and wire diameter will vary with fire size and flow behavior.
  • the screen's grid size may vary from about 0.1 mm to about 30 mm and wire diameters may vary from about 0.1 mm to about 0.8 mm.
  • the method and device described may be used to control and suppress many different types of fires.
  • Typical fires that may be controlled using the invention include localized small fires, residential pool fires, residential and office building fires, aircraft and automobile fires, oil-well fires, fires on waters, fuel tank fires, oil spill fires, and wildfires including forests and grasslands.
  • a further advantage of the present invention is that the catalytic combustion utilized by the methods and devices of the present invention produces relatively low pollutants as compared to sooty natural fires.

Landscapes

  • Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Business, Economics & Management (AREA)
  • Emergency Management (AREA)
  • Catalysts (AREA)

Abstract

The present invention contributes a novel device and method of controlling fire growth by diverting the heat release site from the flame zone to an easily extinguishable catalytic surface. The invention introduces a screen or mesh having a catalytic coating into a flame and causes severe flame instability. The catalytic surface of the screen has a significantly lower activation energy than the flame zone. Therefore, upon insertion of the catalytic screen into the flame plume, the heat release site transitions from the flame zone to the catalytic screen, and the glowing surface of the screen replaces the violent fire plume above a burning object. Because the glowing surface is less violent and combustion occurs at a much lower temperature, the fire is prevented from propagating to nearby structures. Further, without the strong buoyancy forces of hot gases rising upward and flame being augmented by crosswinds, the glowing surface of the catalytic screen is readily extinguished.

Description

BACKGROUND OF THE INVENTION
This invention relates to a device and method of suppressing fire plumes above combustible structures. More particularly, the present invention relates to controlling and suppressing fires by inserting a catalytic screen into the fire and diverting the reactions from the violent flame zone to a silent catalytic solid surface.
When a flaming combustion starts, the hot flame above the burning object acts as an aerodynamically strong diffusion pump powered by natural buoyancy forces. Ambient air is entrained along the boundary of the flame because of the upward movement of hot combustion gases caused by the large buoyancy forces. The violence of the fire thus depends on the buoyancy force generated by hot gases rising above the fire and the ambient air rushing into the fire. More often than not, crosswinds augment the fire violence. In time, the flame turns into a propagating large-scale fire with ever increasing strength and ability to destroy nearby combustible objects. Out of control fires cause severe threats to both life and property at an ever increasing rate. Thus, a critical need exists for newer and more efficient fire control methods.
Current methods used to suppress fires of various magnitudes include cooling the fire by water mist, blanketing oxygen influx by using heavy gases such as carbon dioxide and foam, and inhibiting chain-branching chemical reactions in the flame by using chemical additives. Chemical additives include, but are not restricted to, the halons CF2Br2 and CF2BrCl, and certain dry powders. Additionally, some explosive reactions are used to aerodynamically blow off the flame and assist in suppressing the fire.
The degree of success achieved in these methods depends on the specific fire scenario at hand. The prior art methods are known to present serious limitations under various fire scenarios. For instance, the water spray methodology of controlling fires is the most widely used, but the water mist is often incapable of penetrating against the upward fire flow into the surface to cool the fire. In addition, chemical additives are not always effective, and they pose pollution problems that may be caused by their use in controlling fires. Therefore, suppression of wild fires and uncontrolled fires generally continues to be difficult, especially for very violent fires of great strength having strong upward flow of hot combustion gases.
Some attempts have been at using some type of screen or mesh covering inside fire plumes to assist in controlling fire. However, previous studies reporting the effect of including non-catalytic screens inside fire plumes indicate that screens provide little assistance in suppressing a flame. In a journal article, T. Log and G. Heskestad, Fire Safety Journal, volume 31, 1998, describe variations of flame properties upon introducing a non-catalytic metal screen into the flame. The authors report a net increase in time-averaged flame temperatures. The placement of an inert surface inside a flame did not change the overall chemistry and dynamics of the flame.
U.S. Pat. No. 5,158,144 issued to Mark D. Shaw and Laurence M. Bierce on Oct. 27, 1992 teaches a method of creating a non-burning zone at the flame base by introducing a non-catalytic metal mesh or screen. By constantly raising the screen, a distance of free flowing fuel without fire can be created below the flame. The screen thus prevents the fire from burning below it mainly due to the aerodynamic effect. However the screen does not modify the properties of the flame burning above the screen.
Accordingly, it would be highly desirably to provide a method for using a screen or mesh for suppressing fire that would modify the flame properties such that the flame would be easily extinguished.
Certain combustion catalysts are known to create reactive surface sites by significantly reducing the activation energy of combustion reactions. Several theories have been proposed for the combustion and ignition of hydrocarbon fuels in the presence of noble metal catalysts as early as the 1970s and 1980s. The catalytic ignition behavior of a fuel- air system depends on the nature of catalysts, their effective surface area, and fuel-air equivalence ratios.
Applications for catalytic combustion technology exists in several camping accessories, household appliances and industrial combustion systems. In these existing applications, catalytic combustion technology is used to replacing flaming combustion with catalytic radiant glow to create flameless combustion applications for cooking, heating, and improving efficiency. However, prior art does not exist with respect to the application of catalytic combustion technology for suppressing and controlling violent fires.
SUMMARY OF THE INVENTION
The inventor has found that flaming gas phase combustion will transition to glowing surface combustion in the presence of a significantly lower activation energy catalytic surface. In the present invention, a fire is controlled by transforming the gas phase combustion of a violent flame into a surface catalytic combustion process, thus weakening or eliminating the violent fire plume above the burning structures.
The gas phase ignition temperature of a combustible mixture containing a gaseous fuel and air is generally above 1000° C. However, in the presence of a suitable catalytic surface, the fuel-air mixture can ignite at a much lower temperature because of lower activation energy of combustion. The ignition temperature can be as low as 400-500° C. depending on the nature of the catalyst. When the catalyst is heated to above its activation temperature, combustion reactions occur on the surface, resulting in a glowing surface. As the surface combustion becomes more efficient, the flame above the burning surface becomes weaker and unstable. At high enough catalytic combustion rates, the flame will disappear and leave behind a glowing surface, thus preventing the fire from propagating to nearby structures. Because of the near absence of a strong fire plume above the burning objects, a conventional sprinkler system can be easily used to cool the surface.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 depicts a typical fire plume above a burning object.
FIG. 2a illustrates a catalyst coated mesh screen of the present invention inserted at the flame base and having a reduced flame and a glowing surface.
FIG. 2b illustrates a cut-away top view of a catalyst coated mesh screen as shown in FIG. 2a inserted at the flame base and having a reduced flame and a glowing surface.
FIG. 3a and FIG. 3b illustrate a catalyst coated mesh screen of the present invention inserted at the flame base and having a glowing surface.
FIG. 4 illustrates multiple screens stacked onto a flame base.
FIG. 5 shows a plurality of screens spread over a flame base to cover a wider area of fire.
FIG. 6 illustrates a catalyst coated screen of the present invention having a mesh structure with impermeable regions.
FIG. 7 illustrates a honeycomb substrate structure coated with catalysts as an alternative embodiment of the present invention.
FIG. 8 illustrates as an alternative embodiment of the present invention a combination of a mesh catalyst screen structure and a honeycomb substrate structure coated with catalysts.
FIG. 9 illustrates a means of inserting the catalyst coated screen into a flame base.
DETAILED DESCRIPTION OF THE INVENTION
FIG. 1 shows a fire plume 2 established above a burning object 4. The burning object 4 is also considered a source 4 of fuel gas flow 6. The source 4 can be either gas or gaseous products produced from a condensed phase. The condensed phase includes solids, liquids, or a combination thereof. The fuel vapors from the burning object 4 rise into the upward flowing fire region as shown by fuel flow 6 and keep the fire 2 burning.
The air entrainment process 8 in a typical fire plume 2 is indicated in FIG. 1 by a downward arrow 8. The flow inside a moderate and large-scale fire 2 is highly turbulent. Air and fuel vapors meet and burn instantaneously at locations 10 at the fire's boundaries as a diffusion flame. The combustion process in fires is usually diffusion-controlled. Chemical reaction rates are generally high. The hot gas phase above the fuel source 4, referred to as fire 2, is generally about 1600-2000° C. Depending on the fire size and crosswind conditions, the fire 2 moves violently at all sides and attempts to bounce onto nearby combustible objects.
In the present invention, a mesh material or a screen 12 is placed across the base 14 of the fire as shown in FIG. 2a and FIG. 2b. The screen 12 is coated with a catalytic material and is also referred to as a catalytic screen, catalytic screening member, or a fire-suppression screen 12. The catalyzing process begins, and the screen 12 quickly heats up to its activation temperature, which is lower because of the catalytic coating. The fuel-air mixture ignites at a temperature as low as 400-500° C. because of lower activation energy caused by the combustion catalyst. When the catalyst is heated to above its activation temperature, combustion reactions occur on the surface of the screen 12.
The catalytic screen member 12 is heated to its activation temperature during its descent to the fire's base 14. Thus, the catalytic screen 12 is immediately hot enough to cause surface combustion reactions and begin the transition to surface glow. When the flame boundary meets the screen 12 at reaction point 16, the oxygen of the air entrainment process 8 and fuel vapor of the fire 2 react and release heat producing a glow as shown at the reaction point 16. Both the reduced flame 18 and initial glow reaction 16 are seen immediately after inserting the screen 12. Initially, the glowing region follows the shape of the fuel as shown by reaction point 16 in FIG. 2b. This is because the oxygen and fuel meet the screen 12 at the locations where the temperature of the screen 12 is above the catalyst activation temperature. At the center of the screen 12, a weak flame 18 may persist. If the screen 12 is fine enough, the fuel flow 6 will be partially blocked from rising above, and the flow will go sideways and meet the oxygen at the edge of the screen 12.
FIG. 3a and FIG. 3b show the transition from the residual fire 18 in FIG. 2a to a glowing surface 20 with a temperature about 1000° C. The placement of the catalyst coated screen 12 into the base 14 of the fire plume 2 causes the fire 2 to transition into a glow 20 that replaces the fluid dynamically strong, and violent fire plume 2 depicted FIG. 1. Because the glow is less violent, the reaction event is much safer and manageable. Primarily, the glow will not ignite nearby objects as a violent flame 2 will. Further, the glow 20 is easily extinguished by cooling the glowing surface with a standard system of dispensing water onto the surface. Alternatively, other fire extinguishing chemicals, fluids, solids, or methods may be applied to the glow 20 and will generally be highly successful in extinguishing the non-violent glowing surface.
In order to divert the upward bulk flow 6 through the center of the screen 12 as shown in FIG. 2b, multiple screens may be necessary. FIG. 4 describes a typical multiple mesh system 22 to obtain an effective transition from fire 2 to surface glows 20. The physical size of the screen 12 and its orientation depends on the fire scale and intensity. In FIG. 4 several screens including a catalytic screen 28 and non-catalytic screen 30 are shown stacked vertically. The vertically stacked arrangement of multiple screens may be useful in cases of fires 2 having very strong upward flow 6. The vertically stacked screens will provide several reactive surfaces such as the reactive surfaces 16 in FIG. 2b. Multiple reactive surfaces may assist in controlling the fire 2 and causing the fire 2 to transition into catalytic surface glow 20 on the screens.
In addition to the catalyst coated mesh 28 in the multiple mesh system 22, the alternate mesh 30 may be a simple mesh without a catalytic coating. In addition, random patches of impermeable regions 32 may be used on a mesh as shown in FIG. 6 to block the upward flow 6 and accelerate the transition to surface glow.
Alternatively, a honeycomb structure 24 may be used as shown in FIG. 7. The depth of the honeycomb channel 26 in FIG. 7 may be suitably dimensioned to get an optimum fire transition result. It is also possible to use a combination of a screen 28 and a honeycomb structure 24 as shown in FIG. 8.
The position and dimensions of the screen 12 are optimized for each fire scenario based on the magnitude of the area and flow 6 of the fire 2. Depending on the area of the fire source 4, several units of individual screens 12 may be combined and linked together as illustrated by FIG. 5. The screens 12 may be retained against the fire base 14 by their own weight, or further support may be added depending on the specific fire scenario. In suitable cases, weights 18 may be added to hold the screen 12 in place against the upward fire flow 6. Various wheels and pulleys and equipment such as cranes, lifts, or aircraft may be used to position screens in certain fire scenarios. A possible scenario using an aircraft 34 to place multiple catalytic screening members 12 at the source 4 of a wildfire 2 is illustrated in FIG. 9.
The catalyst and substrate combined form a fire screening member 12 for insertion into a fire plume 2. Catalytic materials for coating the screen 12 may include platinum, palladium and their alloys, transition metal oxides, and other low temperature oxidation catalysts. The alloys of the these metals may be used for more effective catalyst performance. A catalyst having a composition with an extremely low activation or light off temperature is desirable to cause a quicker transition from fire to glow. The surface reactions caused by the combustion catalyst may be further accelerated by supplying additional air or oxidizing chemicals to the surface of the catalytic screen 12.
These catalysts are coated on a substrate material or screen 12 of sufficient mechanical strength. The substrates may also be called catalyst support materials. Preferably, the catalyst will very thinly coated on the substrate. A thin coating of the catalyst is still be effective and cost efficient. The known process of modem chemical vapor deposition (CVD) or any other thin-coating method may be utilized to formulate an efficient catalytic screen. After a reasonable number of fire control applications, the catalytic surface of the screening member is regenerated. Similarly, after the catalytic surface become ineffective, it may be re-coated with the catalyst.
Typical substrates may include metal screens or meshes, honeycomb structures, or a foam-like network. Other non-combustible materials and fibers that may be used as substrates include ceramic foam, a non-oven carbon mat, graphitic felt, carbon fiber yarn, carbon felt, woven ceramic fibers, fiberglass mats, and monoliths, also referred to as honeycombs. Various substrates may be used and the list provided is not intended to be all inclusive. In some cases, the substrate and catalyst of the screening member may be combined or the same material rather than having a substrate that is coated by a separate catalytic material. Obvious variations and combinations of both catalytic coatings and substrates will become apparent to those skilled in the art. Typically, preferred embodiments of the invention will consist of very fine stainless steel screens of grid size 0.1 mm and wire diameter 0.2 mm. The preferred grid size and wire diameter will vary with fire size and flow behavior. The screen's grid size may vary from about 0.1 mm to about 30 mm and wire diameters may vary from about 0.1 mm to about 0.8 mm.
The method and device described may be used to control and suppress many different types of fires. Typical fires that may be controlled using the invention include localized small fires, residential pool fires, residential and office building fires, aircraft and automobile fires, oil-well fires, fires on waters, fuel tank fires, oil spill fires, and wildfires including forests and grasslands. A further advantage of the present invention is that the catalytic combustion utilized by the methods and devices of the present invention produces relatively low pollutants as compared to sooty natural fires.
It will be obvious to those skilled in the arts that substitutions and equivalents will exist for the elements of the embodiment illustrated above. The true scope and definition of the invention, therefore, is to be as set forth in the following claims.

Claims (29)

I claim:
1. A method of controlling fire comprising the steps of providing a catalytic screening member, providing a combustion catalyst on a surface of the catalytic screening member, and placing the catalytic screening member into a flame causing said flame to transition into a glowing surface.
2. A method of controlling a fire as claimed in claim 1, further including the step of extinguishing said glowing surface.
3. A method of controlling a fire as claimed in claim 2 in which said step of extinguishing said glowing surface includes applying water to said glowing surface.
4. A method of controlling a fire as claimed in claim 2 in which said step of extinguishing said glowing surface includes subjecting said glowing surface to crosswinds.
5. A method of controlling fire as claimed in claim 1 in which said catalytic screening member is comprised of stainless steel and the step of providing a combustion catalyst on the surface of the catalytic screening member includes coating the surface of the catalytic screening member with the combustion catalyst.
6. A method of controlling a fire as claimed in claim 5 in which said stainless steel screen has a grid size of 0.1 mm and a wire diameter of 0.2 mm.
7. A method of controlling fire as claimed in claim 1, further including the step of supplying a supplemental flow of oxygen to said catalytic screening member to facilitate the transition into said glowing surface.
8. A method of controlling fire as claimed in claim 1, further including the step of supplying an oxidizing chemical to said catalytic screening member to facilitate the transition into said glowing surface.
9. A method of controlling fire as claimed in claim 1, further including the step of providing a non-catalytic screening member and in which said catalytic screening member and the non-catalytic screening member are placed into said flame by stacking the catalytic screening member and the non-catalytic screening member vertically.
10. A method of controlling a fire as claimed in claim 1 in which the step of supporting the combustion catalyst on the catalytic screening member includes coating the catalytic screening member with the combustion catalyst.
11. A method of controlling a fire as claimed in claim 1 in which the combustion catalyst is either platinum or palladium and their alloys.
12. A method of controlling fire comprising the steps of providing a catalytic screening member, providing a substrate supporting a catalyst on the catalytic screening member and placing the catalytic screening member into a flame causing said flame to transition into a glowing surface.
13. A method of controlling a fire as claimed in claim 12 in which said catalyst is either platinum or palladium and their alloys.
14. A method of controlling a fire as claimed in claim 12 in which said catalyst is a transition metal oxide.
15. A method of controlling fire as claimed in claim 12 in which said catalyst is coated onto said substrate using modem chemical vapor deposition.
16. A device for controlling a fire having a flame plume and a base, comprising a catalytic screen member formed of a substrate having at least one surface thereof coated by a catalyst.
17. A device for controlling a fire as claimed in claim 16 in which said substrate is a mesh screen.
18. A device for controlling a fire as claimed in claim 16 in which said substrate is a foam sheet.
19. A device for controlling a fire as claimed in claim 16 in which said substrate is a screen made of stainless steel.
20. A device for controlling a fire as claimed in claim 16 in which said substrate is a honeycomb sheet.
21. A device for controlling a fire as claimed in claim 16 which said substrate consists of non-combustible fibers.
22. A device for controlling a fire as claimed in claim 16 in which said catalyst is a transition metal oxide.
23. A device for controlling a fire as claimed in claim 16 in which said substrate includes impermeable areas to achieve a desired flow resistance.
24. A device for controlling a fire having a flame plume and a base, comprising a catalytic screen member formed of a substrate having at least one surface thereof coated by a catalyst in which the catalyst is either platinum or palladium and their alloys.
25. A device for controlling a fire having a flame plume and a base, comprising multiple screen members with at least one screen member having a catalytic surface supporting a combustion catalyst.
26. A device as claimed in claim 25 including a means for linking said screen members together to cover a larger area of said fire.
27. A device as claimed in claim 25 in which said screen members are stacked vertically for controlling said fire.
28. A device as claimed in claim 25 including at least one screen member having a non-catalytic surface.
29. A device for controlling a fire having a flame plume and a base, comprising a catalytic screen member having a surface thereof coated by a combustion catalyst in which the combustion catalyst is coated onto the surface using chemical vapor deposition.
US09/634,622 2000-08-05 2000-08-05 Device and method for controlling fire Expired - Fee Related US6474420B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US09/634,622 US6474420B1 (en) 2000-08-05 2000-08-05 Device and method for controlling fire

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US09/634,622 US6474420B1 (en) 2000-08-05 2000-08-05 Device and method for controlling fire

Publications (1)

Publication Number Publication Date
US6474420B1 true US6474420B1 (en) 2002-11-05

Family

ID=24544562

Family Applications (1)

Application Number Title Priority Date Filing Date
US09/634,622 Expired - Fee Related US6474420B1 (en) 2000-08-05 2000-08-05 Device and method for controlling fire

Country Status (1)

Country Link
US (1) US6474420B1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20020050534A1 (en) * 2000-10-30 2002-05-02 The United States Of America Represented By The Secretary Of The Navy Textile and cordage net fire extinguisher system
US20070158084A1 (en) * 2005-11-28 2007-07-12 Protektor Innovations Inc. Deployable fire extinguishing towel
US8297371B1 (en) 2008-04-29 2012-10-30 Musser Jr John E System and methods for fire protection

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4361190A (en) * 1979-09-07 1982-11-30 Vulcan Industrial Packaging Limited Method and apparatus for providing a traversable pathway through a pool of flammable fluid
US4602611A (en) * 1985-09-16 1986-07-29 Hankey Dana L Snuffer for kitchen fires
US5158144A (en) 1991-04-12 1992-10-27 Shaw Mark D Device and method to extinguish oil well fires
US5738175A (en) 1988-12-06 1998-04-14 Alhamad; Ghaleb Mohammad Yassin Compositions of matter for stopping fires, explosions and oxidations of materials and build up of electrostatic charges and method and apparatus for making same
US6048805A (en) * 1997-05-23 2000-04-11 No Fire Technologies Inc. Fire, heat and backdraft protection shield for firefighters
US6062316A (en) * 1988-12-06 2000-05-16 Alhamad; Shaikh Ghaleb Mohammad Yassin Compositions of matter for stopping fires, explosions and oxidations of materials and build up of electrostatic charges

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4361190A (en) * 1979-09-07 1982-11-30 Vulcan Industrial Packaging Limited Method and apparatus for providing a traversable pathway through a pool of flammable fluid
US4602611A (en) * 1985-09-16 1986-07-29 Hankey Dana L Snuffer for kitchen fires
US5738175A (en) 1988-12-06 1998-04-14 Alhamad; Ghaleb Mohammad Yassin Compositions of matter for stopping fires, explosions and oxidations of materials and build up of electrostatic charges and method and apparatus for making same
US6062316A (en) * 1988-12-06 2000-05-16 Alhamad; Shaikh Ghaleb Mohammad Yassin Compositions of matter for stopping fires, explosions and oxidations of materials and build up of electrostatic charges
US5158144A (en) 1991-04-12 1992-10-27 Shaw Mark D Device and method to extinguish oil well fires
US6048805A (en) * 1997-05-23 2000-04-11 No Fire Technologies Inc. Fire, heat and backdraft protection shield for firefighters

Non-Patent Citations (6)

* Cited by examiner, † Cited by third party
Title
K.C. Adiga, D.E. Ramaker, P.A. Tatem, and F.W. Williams, Numerical Predictions for a Simulated Methane Fire, Fire Safety Journal, 1990, pp. 443-458, vol. 16.
M.A. Delichatsios, Air Entrainment into Buoyant Jet Flames and Pool Fires, Combustion and Flame, 1987, pp. 33-46, vol. 70.
M.R. Dongworth and A. Melvin, Diffusive Catalytic Combustion, Proceedings, 16th Symposium (International) on Combustion, The Combustion Institute, Pittsburgh, P.A., 1976, pp. 255-264.
R.K. Lyon and J.A. Cole, Unmixed Combustion: An Alternative to Fire, Combustion & Flame, 2000, pp. 249-261, vol. 121.
T. Griffin and L.D. Pfefferle, Gas Phase and Catalytic Ignition of Methane and Ethane in Air over Platinum, Aiche Journal, 1990, p. 861, vol. 36 No. 6.
T. Log and G. Heskestad, Temperatures of Restricted Turbulent Fire Plumes, Fire Safety Journal, 1998, pp. 101-115, vol. 31.

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20020050534A1 (en) * 2000-10-30 2002-05-02 The United States Of America Represented By The Secretary Of The Navy Textile and cordage net fire extinguisher system
US6695068B2 (en) * 2000-10-30 2004-02-24 The United States Of America As Represented By The Secretary Of The Navy Textile and cordage net fire extinguisher system
US20070158084A1 (en) * 2005-11-28 2007-07-12 Protektor Innovations Inc. Deployable fire extinguishing towel
US8297371B1 (en) 2008-04-29 2012-10-30 Musser Jr John E System and methods for fire protection

Similar Documents

Publication Publication Date Title
US5993192A (en) High heat flux catalytic radiant burner
EP0694735B1 (en) Combustive destruction of noxious substances
CN105899876B (en) For operate include hole flame holder combustion system method
US5419121A (en) Method and apparatus for reduction of pollutants emitted from automotive engines by flame incineration
US3057400A (en) Glow burner for fuel-air mixture
JPH0611120A (en) Low nox forming gas burner device and method thereof
CN108291717A (en) Perforation flame holder with gap between ceramic tile group
CN107795992A (en) Complex burner with velocity compensation mesh and thickness
GB1591302A (en) Fluidised bed
US3245459A (en) Catalytic heater and catalyst therefor
EP1898153B1 (en) Gas burner for cooking appliances
JP3071833B2 (en) Catalytic combustion device
KR20100098632A (en) Flameless thermal oxidation apparatus and methods
US6474420B1 (en) Device and method for controlling fire
AU3000501A (en) Method and device for simulating the rapid spread of flames
NO318705B1 (en) Process and reactor for combustion of fuels
GB2220410A (en) Apparatus for preparing oxygen
MXPA01000808A (en) Air inlets for gas water heaters.
US3833336A (en) Remote fire stack igniter
JP4917548B2 (en) Burner combustion efficiency improvement device
Schwartz et al. Flares
CA2625935C (en) Self-extinguishing relightable wick for use on candles and the like
RU2094703C1 (en) Surface-combustion gas burner
CN117419348B (en) Gas diffusion ignition torch
US6578531B1 (en) Gas appliance with flash suppressor

Legal Events

Date Code Title Description
REMI Maintenance fee reminder mailed
FPAY Fee payment

Year of fee payment: 4

SULP Surcharge for late payment
REMI Maintenance fee reminder mailed
FPAY Fee payment

Year of fee payment: 8

SULP Surcharge for late payment

Year of fee payment: 7

REMI Maintenance fee reminder mailed
LAPS Lapse for failure to pay maintenance fees
STCH Information on status: patent discontinuation

Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362

FP Lapsed due to failure to pay maintenance fee

Effective date: 20141105